Corrosion Inhibition and Adsorption Properties of 1-Methyl Imidazole on Mild Steel in Binary Acid Mixture of (HNO3+HCl)

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1 IJAPC Vol. 3(3), July - Sep, 2014 ISSN: INTERNATIONAL JOURNAL OF ADVANCES IN PHARMACY, IOLOGY AND CHEMISTRY Research Article Corrosion Inhibition and Adsorption Properties of 1-Methyl Imidazole on Mild Steel in inary Acid Mixture of (HNO3+HCl) K.. Patel*, H. K. Kadiya 1. * 1 C. U. Shah Science College, IncomeTax, Ahmedabad, Gujarat-India. ASTRACT 1-Methyl imidazole (N-Methyl imidazole) is tested as corrosion inhibitor on Mild Steel in (HNO 3 + HCl) binary acid mixture by different methods. The inhibition action depends on the chemical structure, concentration of the inhibitor and concentration of the corrosive medium.many N-hetero cyclic compounds with polar groups and/or π electrons are acting as efficient corrosion inhibitors in acidic solutions. Results obtained from weight loss method, temperature effect method and polarization technique revealed that N-hetero cyclic compound 1-Methyl imidazole act as good inhibitor on Mild Steel in (HNO 3 + HCl) binary acid mixture. Corrosion rate increases with rise in temperature and with rise in concentration of mix acid. Inhibition efficiency increases with rise in the concentration of inhibitor. Different values like activation energy, heat of adsorption, enthalpy of adsorption, entropy of adsorption etc. were calculated. Key Words: Corrosion, Mild Steel, Nitric acid, Hydrochloric acid, 1-Methyl imidazole. INTRODUCTION Mild steel is widely employed in industry because of its low cost and availability. Acid solutions are generally used for the removal of undesirable scale and rust in several industrial processes. Inhibitors are generally used to control metal dissolution. The inhibition of corrosion in acid solutions can be secured by the addition of a variety of organic compounds and has been investigated by several workers 1-4. Most of the well known acid inhibitors are organic -compounds containing O, S and/or N atoms 5,6. Aliphatic amines, heterocyclic amines, aromatic amines and phenolic compounds have been extensively investigated as corrosion inhibitors In this paper, the role of 1-Methyl imidazole in inhibiting the corrosion of Mild steel in (HNO 3 + HCl) binary acid mixture has been reported. MATERIALS AND METHODS The mild steel used had the following chemical composition (0.025% C, 0.013% Si, 0.010% S, 0.014% P, 0.210% Mn, 0.008% Ni, 0.007%Cr, 0.002% Mo, 0.006% Cu, 0.059% Al and balance Fe). Rectangular specimens of Mild Steel of size (5.10 cm x 2.04 cm x 0.12 cm thickness) with a small hole of ~2 mm diameter just near one end of the specimen were used for the determination of corrosion rate. All the specimens were cleaned by buffing and wrapped in plastic bag to avoid atmospheric corrosion. A specimen, suspended by a glass hook, was immersed in 200 ml of three different concentration test solution at 300 ± 1 K for 24 h. After the test, the specimens were cleaned by using wash solution prepared by adding 2% Sb 2 O 3 (antimony Oxide), 5% SnCl 2 (stannous chloride) in concentrated HCl (100 ml) at room temperature with constant stirring about mins 14,15, washed with water, acetone and dried in air. To study the effect of temperature on corrosion of Mild Steel in binary acid mixture (0.05 M HNO M HCl), the specimens were immersed in 200 ml of corrosive solution and corrosion rate was determined at various temperatures e.g. at 300, 310, 320 and 330 K for an immersion period of 3hr with and without inhibitor. From the data, I.E.(in %), 538

2 energy of activation (Ea), heat of adsorption (Qads), free energy of adsorption (ΔG 0 ads), change of enthalpy (ΔH 0 ads) and entropy of adsorption (ΔS 0 ads) were calculated. For polarization study, metal specimen having an area of dm 2 was used. Corrosion behavior of Mild steel samples were tested in ( 0.05M HNO M HCl ) & (0.05M HNO M HCl) + 1-Methyl imidazole solutions using potentiostat Gamry Reference 600. Corrosion cell which consists of Calomel electrode as reference electrode, graphite rod as counter electrode and test samples as working electrode. RESULTS AND DISCUSSION The results are given in Tables 1 to 4. To assess the effect of corrosion of Mild steel in (HNO 3 + HCl) binary acid mixture, 1-Methyl imidazole was added as an inhibitor. I.E. was calculated by the following formula. I.E. (%) = [(Wu Wi) / Wu] X (1) Where, Wu is the weight loss of metal in uninhibited acid and Wi is the weight loss of metal in inhibited acid. Energy of activation (Ea) has been calculated with the help of the Arrhenius equation [16]. log (ρ 2 / ρ 1 )= Ea/ R [(1/T 1 ) (1/T 2 )] (2) Where ρ 1 and ρ 2 are the corrosion rate at temperature T 1 and T 2 respectively. The values of heat of adsorption (Qads) were calculated by the following equation [16]. Qads = R [log (θ 2 / 1 θ 2 ) - log ( θ 1 / 1 θ 1 )] x [T 1. T 2 / T 2 T 1 ] -----(3) Where, θ 1 and θ 2, [θ = (Wu Wi) / Wi] are the fractions of the metal surface covered by the Inhibitors at temperature T 1 and T 2 respectively. The values of the free energy of adsorption (ΔG 0 ads) were calculated with the help of the following equation [17]. log C = log ( θ / 1 θ ) log -----(4) Where, log = 1.74 ( G 0 a / RT) and C is the inhibitor concentration. The enthalpy of adsorption (ΔH 0 ads) and entropy of adsorption (ΔS 0 ads) are calculated using the following equation [18]. ΔH 0 ads = Ea RT (5) ΔS 0 ads = [ΔH 0 ads - ΔG 0 ads] / T (6) Table-1 shows that corrosion rate increases with increase in concentration of mix acid while % of I.E. decreases. Also as concentration of inhibitor increases corrosion rate decreases while % of I.E. increases. Table-2 shows that as the temperature increases, Corrosion rate increases while % of I.E. decreases. Mean Ea values were calculate by using equation 2 for mild steel in 0.05 M inary acid mixture is KJMol -1 while acid containing inhibitors the mean Ea values were found to be higher than that of uninhibited system (table 2). The higher values of mean Ea indicate physical adsorption of the inhibitors on metal surface. From Table-3 it is evident that the values of Qads were found to be negative and lies in the range of to KJMol -1. Oguzje explained that the degree of surface coverage decreased with rise in temperature 19. The higher negative values of heat of adsorption also show that the inhibition efficiency decreased with a rise in temperature. From Table-3 the negative mean ΔG 0 ads values ranging from to KJMol - indicate that the adsorptions of the inhibitors are spontaneous. The most efficient inhibitor shows more negative ΔG 0 ads value. This suggests that they are strongly adsorbed on the metal surface. The values of enthalpy changes (ΔH) were positive indicating the endothermic nature of the reaction 20 suggesting that higher temperature favors the corrosion process. The entropy (ΔS) is positive confirming that the corrosion process is entropically favorable 21. Polarization behaviour: Anodic and cathodic polarization curve without inhibitor shown in fig -1 and with inhibitors shown in fig - 2 indicates polarization of both anodes and cathodes. I.E. calculated from corrosion current obtained by extrapolation of the cathodic and anodic Tafel constants are given in Table 4. The I.E. obtained from weight loss and polarization measurement were in fairly good agreement. Mechanism: The mechanism of inhibition of corrosion is generally believed to be due to the formation and maintenance of a protective film on the metal surface. Mild Steel dissolves in (HNO 3 + HCl) acid mixture. CONCLUSION The present study shows that 1-Methyl imidazole is an efficient inhibitor for the corrosion of Mild Steel in (HNO 3 + HCl) binary acid mixture. It appears that an efficient inhibitor is characterized by negative 539

3 value of free energy of adsorption, positive value of entropy of adsorption and higher (more negative) heat of adsorption.corrosion rate increases with increase in the concentration of binary acid mixture. Inhibition efficiency increases with increase in concentration of 1-Methyl imidazole. ACKNOWLEDGEMENT The authors are thankful to Department of Chemistry, C. U. Shah Science College, Ahmedabad for providing laboratory facilities. Table - 1 Corrosion Rate (CR) and Inhibition efficiency (I.E.) of Mild Steel in 0.01M, 0.05M, and 0. 1M binary acid mixture ( HNO 3 + HCl ) containing 1-Methyl imidazole as inhibitors for an immersion period of 24 hr at 300 ± 1 K Inhibitor Conc. (%) Acid Concentration 0.01 M 0.05 M 0.1 M CR mg/dm 2 IE % CR mg/dm 2 IE % CR mg/dm 2 IE % A A = ( HNO 3 + HCl ), = ( HNO 3 + HCl ) + 1-Methyl imidazole Table -2 Effect of temperature on corrosion rate (CR), inhibitive efficiency (IE %), energy of activation (Ea) for Mild Steel in 0.05 M binary acid mixture containing inhibitor Inhi. Con. In % Temperature 300 K 310 K 320 K 330 K CR IE % CR IE % CR mg/ dm 2 mg/dm 2 mg/dm 2 IE % CR IE % 300- mg/dm K Energy of Activation (Ea) K KJMol K A A = ( HNO 3 + HCl ), = ( HNO 3 + HCl ) + 1-Methyl imidazole. Mean Ea Table -3 Heat of adsorption (Qads) and free energy of adsorption (ΔG 0 ads) for Mild Steel in 0.05 M binary acid mixture containing inhibitor. Inhibitor Conc. % Heat of Adsorption Qads KJmol -1 Free Energy of Adsorption ΔG 0 ads KJMol K K K 300 K 310 K 320 K 330K Mean ΔG 0 ads A A = ( HNO 3 + HCl ), = ( HNO 3 + HCl ) + 1-Methyl imidazole. 540

4 Table - 4 Polarization data and Inhibition efficiency (IE %) of 1-Methyl imidazole for Mild Steel in (0.05 M HNO M HCl ) at 300 ± 1 K with 1% inhibitor concentration Icorr (ma/sq.cm) Ecorr (mv) Tafel Slope (mv/decade) IE( in %) from methods Anodic βa Cathodic -βc A mv y polarization A = (HNO 3+HCl), = (HNO 3+HCl) + 1-Methyl imidazole, βa = Anodic Tofel constant, βc = Cathodic Tofel constant, (mv) = βa* βc/2.3(βa+ βc) Weight Loss Figure-1 Polarization curve for corrosion of Mild Steel in (0.05 M HNO M HCl ) mix acid in absence of inhibitor Figure-2 Polarization curve for corrosion of Mild Steel in (0.05 M HNO M HCl ) mix acid containing 1% inhibitor concentration 541

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